The effect of the skin-zone on non-Newtonian oil fields

Автор: Dadash-zade M.A., Mirzoyev E.A.

Журнал: Мировая наука @science-j

Рубрика: Основной раздел

Статья в выпуске: 3 (72), 2023 года.

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This article shows the properties of non-Newtonian fluids, examines the causes of the skin zone, and considers the effect of the skin factor depending on the value it receives. Most of the recently put into operation oil fields are non-Newtonian. The presence of substances such as asphaltene, tar, and paraffin in the fluids of such deposits makes it difficult to filter them and increases the costs of their operation and transportation. The formation of a skin zone can lead to a decrease in production in such oil fields. Thus, at positive skin values, a decrease in permeability and well production is observed.

Non-newtonian fluids, skin factor, productivity, formation permeability, formation, pressure drop

Короткий адрес: https://sciup.org/140297329

IDR: 140297329

Текст научной статьи The effect of the skin-zone on non-Newtonian oil fields

Calculation of production of non-Newtonian oil wells

In non-Newtonian oil fields, we can use the following reporting methodology to find and predict the productivity of wells.

We know that the production of wells in operation in anomalous fluid oil fields is calculated using the following formula:

2Trkh[(Pk-Pq)-i0(Rk-Rq)]

*

Here the thickness of h-layer ,k-layer conductivity ,P k - contour pressure , P q -wellbore pressure , R k - the radius of the zone around the well ,R q - the radius of the well ,S-skin factor , ^-dynamic viscosity , i0 = ^=- initial pressure gradient, t 0 -initial touch voltage

It is clear from the equation that R k >>R q . Therefore, it can be ignored in the report:

2nkh [(Pk - Pq) - ioRk] " MH

Now let's run the reports based on the given values:

h=10m, k=0.1*10 -12 m 2 , P k =120*10 5 N/m 2 , P q =80*10 5 N/m 2 , R k =1000 m , i 0 =220 N/m 2 ,μ=15*10 -3 N*s/m 2

Based on the given prices, let's calculate the volume production:

  • 1)    When S=1:

_ 2nkh[(Pk - P q ) - i0Rk^ _ 2 • 3,14 • 0,1 • 10-12 • 10[(120 - 80) • 105 - 220 • 1000]

  • Q       ^[/nR ^ + s]                      15 • 10-3 [Zn^^^ + 1]

= 0.00083 m 3 /s = 71.712 m 3 /day

  • 2)    When S=5:

_ 2тткй[(Р к - P q ) - i 0 R k] _ 2 • 3,14 • 0,1 • 10-12 • 10[(120 - 80) • 105 - 220 • 1000]

  • ^ =           Rk J =                   _ЧГ, 1000 ,

^[Zn-^ + S]                        15^10 3 [/n q +5]

= 0.00056 m3 /s = 48.38 m 3 /day

  • 3)    Let's assume that S=20:

_ 2якЛ[(Р к - P q ) - i 0 R k] _ 2 • 3,14 • 0,1 • 10-12 • 10[(120 - 80) • 105 - 220 • 1000]

  • Q        ^[/nR ^ + s]                      15 • 10-3 [Zn1000 +20]

= 0.00031 m3 /s = 26.78 m 3 /day

Studies show that in most cases, one of the methods used to increase well production is washing the bottom zone with acid. In general, it has been shown in the literature that the amount of acidic solution per 1 meter thickness of the layer is (1.0 ÷ 1.2) m 3 . In this case, the amount of acid:

  • V    = sigh

Then we can use the following expression to find the volume of the acidic solution:

^ k

Xp(5,09XP + 999)

VX k (5,09X k + 999)

Here X is the concentration of the p -acid in the solution

X k -acid (%)

If there is a change in the acid's concentration over time and as the storage conditions change, then the volume of this acid is calculated in the following form:

XP(5,09XP + 999)

  • V L    = V • 5,09 -       ----P

P k( P k - 999)

Here, ρ k is the density of the solution at a temperature of -15 0 C.

P k = P kt + (2,67 • 10-3p kt - 2,52)(t - 15)

  • ρ kt is the density of the acid at a given temperature.

Barium-chlorine is used to neutralize this acid. Its amount is determined by the following expression:

Gbx = 21,3V (a^- 0,02)

Xk

Here a - indicates the volume of sulfuric acid in the total acid. In mining conditions, this amount is calculated as follows:

a = 0,490

Then we can find the volume of barium-chlorine with the following formula:

Ghx

V, x

P bx

Here p xb is the density of barium-chlorine, its value is approximately p xb = 4000 kg/m 3

is accepted. The volume of the inhibitor, in turn, is determined as follows:

  • V [ = b [ ^ Here, b i -inhibitor addition rate. If reagent B-2 was used as an inhibitor, then b i =0.2%. c i is the total volume of inhibitor (c i =100%)

Based on this, we calculate the conditional volume of the solution using the following formula:

- х^хз^ k            27,5(5,09-27,5+999)

Now let's find the density of the given acid at 15 0C:

P15oC = 1134 + (2,67 - 10-3 - 1134 - 2,52)(25 - 15) = 1139.1 kg/m 3

According to the given temperature, the volume of acid is calculated as follows:

V^ = 12,6 5 • 5,0 9 • 135(5,09125+9222= 5.8 m3

K                     1139,1(1139,1-999)

Now let's find the amount of barium chloride:

Gbx = 21,3 • 13,2 • (0,4115 — 0,02) = 49,5kg \     2/,D/

The volume of barium chloride is:

14V = — - 0,0123 « 1,23 • 10-2m 3

°x

Thus, we get the required volume of technical acid:

V = I 1265 = 4,74 • 10-1m 3

Let's calculate the volume of the inhibitor with the help of the formulas mentioned above:

V = 0,2 •1265 = 2,52 • 10-2m3

1       ,      100

Volume of the intensifier:

Vin = 0,3 •1265 = 3,8 • 10-2m3 171

Finally, let's calculate the volume of water required:

V s =12.65-5.82-(0.0123+0.474+0.026+0.0379)=6.28 m3

Список литературы The effect of the skin-zone on non-Newtonian oil fields

  • Assessment of Total Skin Factor in Perforated Wells, Turhan Yildiz, SPE, Colorado School of Mines, February 2006 SPE Reservoir Evaluation & Engineering.
  • Comparison of Skin Factors for Perforated Completions Calculated with Computational Fluid Dynamics Software and a Semi-Analytical Model, Datong Sun, Baoyan Li, Mikhail Gladkikh, Rajani Satti. Randy Evans, SPE, Baker Hughes Incorporated, 2011, Society of Petroleum Engineers.
  • Near Wellbore Damage and Types of Skin Depending on Mechanism of Damage, Mahesh Chandra Patel, and Aaditya Singh, Gubkin Russian State University of Oil and Gas, Moscow,2016, Society of Petroleum Engineers.
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